SU957758A3 - Process for producing silicon dioxide - Google Patents
Process for producing silicon dioxide Download PDFInfo
- Publication number
- SU957758A3 SU957758A3 SU752182607A SU2182607A SU957758A3 SU 957758 A3 SU957758 A3 SU 957758A3 SU 752182607 A SU752182607 A SU 752182607A SU 2182607 A SU2182607 A SU 2182607A SU 957758 A3 SU957758 A3 SU 957758A3
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- hydrogen
- reaction
- flame
- oxygen
- silicon dioxide
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
- C01B13/14—Methods for preparing oxides or hydroxides in general
- C01B13/20—Methods for preparing oxides or hydroxides in general by oxidation of elements in the gaseous state; by oxidation or hydrolysis of compounds in the gaseous state
- C01B13/22—Methods for preparing oxides or hydroxides in general by oxidation of elements in the gaseous state; by oxidation or hydrolysis of compounds in the gaseous state of halides or oxyhalides
- C01B13/30—Removal and cooling of the oxide-containing suspension
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F7/00—Compounds of aluminium
- C01F7/02—Aluminium oxide; Aluminium hydroxide; Aluminates
- C01F7/30—Preparation of aluminium oxide or hydroxide by thermal decomposition or by hydrolysis or oxidation of aluminium compounds
- C01F7/302—Hydrolysis or oxidation of gaseous aluminium compounds in the gaseous phase
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G23/00—Compounds of titanium
- C01G23/04—Oxides; Hydroxides
- C01G23/047—Titanium dioxide
- C01G23/07—Producing by vapour phase processes, e.g. halide oxidation
- C01G23/075—Evacuation and cooling of the gaseous suspension containing the oxide; Desacidification and elimination of gases occluded in the separated oxide
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/12—Surface area
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Geology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Silicon Compounds (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
- Investigating And Analyzing Materials By Characteristic Methods (AREA)
Abstract
Description
Изобретение относитс к способу получени высокодисперсного диоксида кремни , используемого в различных област х техники. Известен способ получени диоксид кремни путем высокотемпературного гидролиза-хлорида кремни в среде кислорода и горючих газов, охлаждени газообразных продуктов гидролиза и последующего выделени высокодисперс ного диоксида кремни с размером час тиц 10-20 мм. Благодар проведению гидролизав атмосфере азота устран ю образование .свободного хлора Щ . Недостатком этого способа вл етс повышенный расход реагентов за счет проведени гидролиза в атмосфере азота. Известен способ 2 получени диоксида кремни путем высокотемпературного гидролиза хлоридакремни в среде, состо щей из водород- и кисло родсодержащих газов, охлаждени газо юбразн.ых продуктов, обработки их вод ным паром и затем азотом и с после дующим отделением диоксида кремни . Получают высокодисперсный продукт с удельной поверхностью 200 и содержанием свободного хлора О,1 вес.% Недостатками известного способа вл етс использование азота и повышенное содержание свободного хлора в продукте. Цель изобретени - снижение содержани хлора в продукте и упрощение способа за счет исключени введени в Процесс азота. Поставленна цель достигаетс тем , что в известном спосЪбе получени диоксида кремни ,, заключающимс в высокотемпературном гидролизе хлорида кремни в среде водород- кислородсодержащих газов, охлаждении газообразных продуктов реакции с последующим отделением диоксида кремни -, перед отделением диоксида кремни газообразные продукты гидролиза охлаждают до 500-650 0 и обрабатывают их водородом. Отличные от прототипа температурный режим охлаждени и операци обработки газообразных продуктов водородом позвол ют снизить содержание свободного хлора в продукте до 0,07% и получить высокодисперсный продукт с удельной поверхностью 200 Mvr. Кроме того, способ позвол ет утилизировать хлористый водород с получением концентрированной сол ми кислоты.This invention relates to a process for the preparation of highly dispersed silicon dioxide used in various fields of technology. A known method for producing silicon dioxide by high-temperature hydrolysis-of silicon chloride in an environment of oxygen and combustible gases, cooling the gaseous hydrolysis products and the subsequent separation of highly dispersed silicon dioxide with a particle size of 10-20 mm. By carrying out the hydrolysis in a nitrogen atmosphere, the formation of free chlorine is eliminated. The disadvantage of this method is the increased consumption of reagents due to hydrolysis under nitrogen. Known method 2 is the production of silicon dioxide by high-temperature hydrolysis of chloride silicon in a medium consisting of hydrogen- and oxygen-containing gases, cooling gas-gas products, treating them with water vapor and then with nitrogen and followed by the separation of silica. A highly dispersed product is obtained with a specific surface of 200 and a content of free chlorine of O, 1 wt.%. The disadvantages of this method are the use of nitrogen and the increased content of free chlorine in the product. The purpose of the invention is to reduce the chlorine content in the product and simplify the process by eliminating the introduction of nitrogen into the process. The goal is achieved by the fact that in the known method of producing silicon dioxide, which consists in high-temperature hydrolysis of silicon chloride in hydrogen-oxygen-containing gases, cooling the gaseous reaction products with subsequent separation of silicon dioxide, before the separation of silicon dioxide, the gaseous hydrolysis products are cooled to 500-650 0 and treat them with hydrogen. The temperature mode of cooling, which differs from the prototype, and the operation of treating gaseous products with hydrogen reduce the chlorine content in the product to 0.07% and obtain a highly dispersed product with a specific surface of 200 Mvr. Furthermore, the method allows utilization of hydrogen chloride to produce concentrated salts of the acid.
При температуре ниже скорость восстановлени хлора водородом невысока , а содержание хлора в продукте повышенное - 6,7%, При температуре свыше расход водорода повышенный вследствие его взаимодействи с 5 кислородом, а содержание хлора в продукте не уменьшаетс . Взаимодействие в газообразных продуктах реакции хло7 ра с водородом целесообразно вести под действием ультрафиолетового света.10At a temperature below, the rate of reduction of chlorine with hydrogen is low, and the chlorine content in the product is elevated - 6.7%. At a temperature above, the hydrogen consumption is increased due to its interaction with 5 oxygen, and the chlorine content in the product does not decrease. The interaction in the gaseous products of the reaction of chlorine with hydrogen should be carried out under the action of ultraviolet light.
Пример. 2.000 кг С1, 648 водорода и 1.900 нм/ч воздуха подают в аэрозольную горелку. 22 водорода подают в кожух горелки. Получают 706 кг/ч высокодис- з персной кремневой кислоты с удельной поверхностью 200 . Количество свободного хлора в реакционном газе 7,5%. Реакционный газ охлаждают до и ввод т в него 70 водорода. .jn Количество свободногоicJlOij снижаетс до 0,07%. Затем,рр }}/:ченную чонкодисперсную SiOj отдел ютЧЬт .реакцион-. ного газа. .%« Example. 2,000 kg of C1, 648 of hydrogen and 1.900 nm / h of air are fed to the aerosol burner. 22 hydrogen is fed to the burner housing. 706 kg / h of highly dispersed persistent silicic acid with a specific surface of 200 are obtained. The amount of free chlorine in the reaction gas is 7.5%. The reaction gas is cooled before and 70 hydrogen are introduced into it. .jn The amount of freeJlOij is reduced to 0.07%. Then, pp}} /: the finely dispersed SiOj is separated by the reaction. foot gas. .% "
П р и м ер, г.. Осуществл ют процесс аналогично пример} 1. бСГнм/ч водорода втвод т в охлщдвнные до 460°С реакционные газы. Количество свободного хлора при этом снижаетс с 7,5 до 6,7%.Example # 1. The process is carried out in a similar manner to Example} 1. b BCG / m of hydrogen is introduced into the reaction gases cooled to 460 ° C. The amount of free chlorine in this case decreases from 7.5 to 6.7%.
Пример 3. Осуществл ют про- цесс аналогично примеру 1, за исклюieHHeM того, что после проведени химического превращени 70 водорода ввод т в охлажденные до бво-с реакционные газы. Количество свободного хлора остаетс неизменным.Example 3. The process is carried out analogously to Example 1, except for the HHeM that after carrying out the chemical transformation 70 hydrogen is introduced into the reaction gases cooled to bWo. The amount of free chlorine remains unchanged.
Предложенный способ позвол ет упростить процесс за счет исключени расхода дополнительных реагентов (вод ной пар, азот).The proposed method allows to simplify the process by eliminating the consumption of additional reagents (water vapor, nitrogen).
Claims (2)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE2533925A DE2533925C3 (en) | 1975-07-30 | 1975-07-30 | Process for the production of finely divided oxides of metals and / or silicon |
Publications (1)
Publication Number | Publication Date |
---|---|
SU957758A3 true SU957758A3 (en) | 1982-09-07 |
Family
ID=5952748
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU752182607A SU957758A3 (en) | 1975-07-30 | 1975-10-23 | Process for producing silicon dioxide |
Country Status (15)
Country | Link |
---|---|
US (1) | US4276274A (en) |
JP (1) | JPS5216497A (en) |
AT (1) | AT339866B (en) |
BE (1) | BE834651A (en) |
CH (1) | CH615892A5 (en) |
DE (1) | DE2533925C3 (en) |
DK (1) | DK145890C (en) |
FI (1) | FI61854C (en) |
FR (1) | FR2319575A1 (en) |
GB (1) | GB1513890A (en) |
IT (1) | IT1047224B (en) |
NL (1) | NL180199C (en) |
NO (1) | NO138996C (en) |
SE (1) | SE410963B (en) |
SU (1) | SU957758A3 (en) |
Families Citing this family (22)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2849851C3 (en) * | 1978-11-17 | 1981-11-05 | Degussa Ag, 6000 Frankfurt | Process for the pyrogenic production of finely divided oxide of a metal and / or a metalloid |
DE2923064A1 (en) * | 1979-06-07 | 1980-12-11 | Degussa | METHOD FOR PRODUCING FINE-PARTICLE OXIDES OF METALS |
DE2923182A1 (en) * | 1979-06-08 | 1980-12-18 | Degussa | METHOD FOR THE PYROGENIC PRODUCTION OF FINE-PARTICLE OXIDE OF A MATAL AND / OR A METALOID |
DE2931585A1 (en) * | 1979-08-03 | 1981-02-12 | Degussa | TEMPERATURE-STABILIZED, PYROGEN-PRODUCED ALUMINUM OXIDE MIXED OXIDE, THE METHOD FOR THE PRODUCTION AND USE THEREOF |
DE3101720C2 (en) * | 1981-01-21 | 1982-11-04 | Degussa Ag, 6000 Frankfurt | Process for removing halogen from the reaction gases in the pyrogenic production of silicon dioxide |
US4801437A (en) * | 1985-12-04 | 1989-01-31 | Japan Oxygen Co., Ltd. | Process for treating combustible exhaust gases containing silane and the like |
DE3611449A1 (en) * | 1986-04-05 | 1987-10-15 | Degussa | BASIC MATERIAL FOR THE PRODUCTION OF CERAMIC MATERIALS |
US4710369A (en) * | 1986-06-10 | 1987-12-01 | Toth Aluminum Corporation | Oxidation method for production of special aluminas from pure aluminum chloride |
US5123836A (en) * | 1988-07-29 | 1992-06-23 | Chiyoda Corporation | Method for the combustion treatment of toxic gas-containing waste gas |
DE4228711A1 (en) * | 1992-08-28 | 1994-03-03 | Degussa | Silicon-aluminum mixed oxide |
US6193795B1 (en) | 1993-08-02 | 2001-02-27 | Degussa Corporation | Low structure pyrogenic hydrophilic and hydrophobic metallic oxides, production and use |
DE19813971B4 (en) * | 1998-03-24 | 2005-12-01 | Heraeus Quarzglas Gmbh & Co. Kg | Process for the cleaning of SiO2 granulation |
US6887566B1 (en) | 1999-11-17 | 2005-05-03 | Cabot Corporation | Ceria composition and process for preparing same |
CA3030383C (en) | 2016-07-29 | 2023-02-21 | Evonik Degussa Gmbh | Method for producing hydrophobic heat insulation material |
WO2018134275A1 (en) | 2017-01-18 | 2018-07-26 | Evonik Degussa Gmbh | Granular thermal insulation material and method for producing the same |
DE102017209782A1 (en) | 2017-06-09 | 2018-12-13 | Evonik Degussa Gmbh | Process for thermal insulation of an evacuable container |
EP3597615A1 (en) | 2018-07-17 | 2020-01-22 | Evonik Operations GmbH | Granular mixed oxide material and thermal insulating composition on its basis |
KR102576553B1 (en) | 2018-07-18 | 2023-09-08 | 에보니크 오퍼레이션즈 게엠베하 | Method for hydrophobizing insulating-material molded bodies based on silica at ambient pressure |
US20230002627A1 (en) | 2020-01-14 | 2023-01-05 | Evonik Operations Gmbh | Silica-based hydrophobic granular material with an increased polarity |
PL3877332T3 (en) | 2020-01-14 | 2022-07-11 | Evonik Operations Gmbh | Fumed silica with modified surface activity |
EP4043398B1 (en) | 2021-02-11 | 2023-06-28 | Evonik Operations GmbH | Silica with reduced tribo-charge for toner applications |
CN116067191B (en) * | 2023-04-06 | 2023-06-23 | 河北鸿科碳素有限公司 | Flue gas cooler of calciner |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US779998A (en) * | 1903-10-24 | 1905-01-10 | Electric Reduction Company Ltd | Process of making hydrochloric acid. |
US1365740A (en) * | 1916-11-22 | 1921-01-18 | Walter O Snelling | Photochemical apparatus |
US3201337A (en) * | 1961-05-12 | 1965-08-17 | Allied Chem | Process for removing hydrogen from chlorine gas |
US3078148A (en) * | 1961-05-26 | 1963-02-19 | Cabot Corp | Process for making titanium dioxide |
GB1121279A (en) * | 1965-07-28 | 1968-07-24 | Degussa | A process for the production of ultra-finely divided oxides |
DE1667448A1 (en) * | 1966-03-30 | 1971-06-16 | Dschagatspanian Rafael Watscha | Process for purifying chlorine from hydrogen |
BE790704A (en) * | 1971-10-28 | 1973-02-15 | Degussa | PROCESS FOR THE MANUFACTURE OF OXIDES FINE |
-
1975
- 1975-07-30 DE DE2533925A patent/DE2533925C3/en not_active Expired
- 1975-10-07 AT AT766175A patent/AT339866B/en not_active IP Right Cessation
- 1975-10-10 DK DK458475A patent/DK145890C/en active
- 1975-10-10 SE SE7511388A patent/SE410963B/en unknown
- 1975-10-17 BE BE6045225A patent/BE834651A/en not_active IP Right Cessation
- 1975-10-17 JP JP50125239A patent/JPS5216497A/en active Granted
- 1975-10-22 GB GB43314/75A patent/GB1513890A/en not_active Expired
- 1975-10-23 SU SU752182607A patent/SU957758A3/en active
- 1975-10-23 IT IT69627/75A patent/IT1047224B/en active
- 1975-10-23 NL NLAANVRAGE7512423,A patent/NL180199C/en not_active IP Right Cessation
- 1975-10-24 FI FI752976A patent/FI61854C/en not_active IP Right Cessation
- 1975-10-29 CH CH1401575A patent/CH615892A5/de not_active IP Right Cessation
- 1975-10-31 NO NO753664A patent/NO138996C/en unknown
- 1975-12-08 FR FR7537496A patent/FR2319575A1/en active Granted
-
1976
- 1976-07-26 US US05/708,776 patent/US4276274A/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
BE834651A (en) | 1976-04-20 |
NO138996B (en) | 1978-09-11 |
JPS5727842B2 (en) | 1982-06-12 |
ATA766175A (en) | 1977-03-15 |
GB1513890A (en) | 1978-06-14 |
CH615892A5 (en) | 1980-02-29 |
DE2533925A1 (en) | 1977-02-17 |
FI61854B (en) | 1982-06-30 |
IT1047224B (en) | 1980-09-10 |
DK145890B (en) | 1983-04-05 |
FI752976A (en) | 1977-01-31 |
DK458475A (en) | 1977-01-31 |
NL180199C (en) | 1987-01-16 |
FR2319575B1 (en) | 1978-12-01 |
FI61854C (en) | 1982-10-11 |
NL7512423A (en) | 1977-02-01 |
NO138996C (en) | 1978-12-20 |
DE2533925C3 (en) | 1980-12-11 |
AT339866B (en) | 1977-11-10 |
FR2319575A1 (en) | 1977-02-25 |
SE410963B (en) | 1979-11-19 |
NL180199B (en) | 1986-08-18 |
NO753664L (en) | 1977-02-01 |
DK145890C (en) | 1983-10-17 |
US4276274A (en) | 1981-06-30 |
DE2533925B2 (en) | 1980-03-13 |
JPS5216497A (en) | 1977-02-07 |
SE7511388L (en) | 1977-01-31 |
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